JPH0753768B2 - Allyl-terminated polyisobutylene polymer and method for producing the same - Google Patents
Allyl-terminated polyisobutylene polymer and method for producing the sameInfo
- Publication number
- JPH0753768B2 JPH0753768B2 JP62259867A JP25986787A JPH0753768B2 JP H0753768 B2 JPH0753768 B2 JP H0753768B2 JP 62259867 A JP62259867 A JP 62259867A JP 25986787 A JP25986787 A JP 25986787A JP H0753768 B2 JPH0753768 B2 JP H0753768B2
- Authority
- JP
- Japan
- Prior art keywords
- allyl
- chloride
- group
- polyisobutylene polymer
- terminated polyisobutylene
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 229920002367 Polyisobutene Polymers 0.000 title claims description 64
- 229920000642 polymer Polymers 0.000 title claims description 29
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 60
- 238000005937 allylation reaction Methods 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 20
- HYWCXWRMUZYRPH-UHFFFAOYSA-N trimethyl(prop-2-enyl)silane Chemical compound C[Si](C)(C)CC=C HYWCXWRMUZYRPH-UHFFFAOYSA-N 0.000 claims description 18
- 239000000460 chlorine Substances 0.000 claims description 16
- NEHMKBQYUWJMIP-UHFFFAOYSA-N chloromethane Chemical compound ClC NEHMKBQYUWJMIP-UHFFFAOYSA-N 0.000 claims description 12
- 125000004432 carbon atom Chemical group C* 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 9
- 239000002841 Lewis acid Substances 0.000 claims description 8
- 150000007517 lewis acids Chemical class 0.000 claims description 8
- 125000000217 alkyl group Chemical group 0.000 claims description 7
- 239000011541 reaction mixture Substances 0.000 claims description 7
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 claims description 6
- 238000005727 Friedel-Crafts reaction Methods 0.000 claims description 6
- 229910052801 chlorine Inorganic materials 0.000 claims description 6
- 229940050176 methyl chloride Drugs 0.000 claims description 6
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 claims description 6
- FAQYAMRNWDIXMY-UHFFFAOYSA-N trichloroborane Chemical compound ClB(Cl)Cl FAQYAMRNWDIXMY-UHFFFAOYSA-N 0.000 claims description 6
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 5
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims description 5
- 150000001875 compounds Chemical class 0.000 claims description 5
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 claims description 4
- 229910000077 silane Inorganic materials 0.000 claims description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 3
- 239000001257 hydrogen Substances 0.000 claims description 3
- 229910052739 hydrogen Inorganic materials 0.000 claims description 3
- HPGGPRDJHPYFRM-UHFFFAOYSA-J tin(iv) chloride Chemical compound Cl[Sn](Cl)(Cl)Cl HPGGPRDJHPYFRM-UHFFFAOYSA-J 0.000 claims description 3
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims description 2
- 229910021627 Tin(IV) chloride Inorganic materials 0.000 claims description 2
- 150000007824 aliphatic compounds Chemical class 0.000 claims description 2
- 125000005234 alkyl aluminium group Chemical group 0.000 claims description 2
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 150000001491 aromatic compounds Chemical class 0.000 claims description 2
- 125000003118 aryl group Chemical group 0.000 claims description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims description 2
- 229910052794 bromium Inorganic materials 0.000 claims description 2
- 229910052736 halogen Inorganic materials 0.000 claims description 2
- 150000002367 halogens Chemical group 0.000 claims description 2
- 229910001507 metal halide Inorganic materials 0.000 claims description 2
- 150000005309 metal halides Chemical class 0.000 claims description 2
- 229910021550 Vanadium Chloride Inorganic materials 0.000 claims 1
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 claims 1
- RPESBQCJGHJMTK-UHFFFAOYSA-I pentachlorovanadium Chemical compound [Cl-].[Cl-].[Cl-].[Cl-].[Cl-].[V+5] RPESBQCJGHJMTK-UHFFFAOYSA-I 0.000 claims 1
- DUNKXUFBGCUVQW-UHFFFAOYSA-J zirconium tetrachloride Chemical compound Cl[Zr](Cl)(Cl)Cl DUNKXUFBGCUVQW-UHFFFAOYSA-J 0.000 claims 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 19
- 125000001309 chloro group Chemical group Cl* 0.000 description 18
- 238000006243 chemical reaction Methods 0.000 description 15
- -1 silyl enol ether Chemical class 0.000 description 11
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 10
- 230000015572 biosynthetic process Effects 0.000 description 10
- 238000006116 polymerization reaction Methods 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- 238000006459 hydrosilylation reaction Methods 0.000 description 6
- 238000003786 synthesis reaction Methods 0.000 description 6
- 229920001400 block copolymer Polymers 0.000 description 5
- 150000003961 organosilicon compounds Chemical class 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 239000004205 dimethyl polysiloxane Substances 0.000 description 4
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 4
- 229920001296 polysiloxane Polymers 0.000 description 4
- 238000000425 proton nuclear magnetic resonance spectrum Methods 0.000 description 4
- 229920006395 saturated elastomer Polymers 0.000 description 4
- KPJKMUJJFXZGAX-UHFFFAOYSA-N 2-chloropropan-2-ylbenzene Chemical compound CC(C)(Cl)C1=CC=CC=C1 KPJKMUJJFXZGAX-UHFFFAOYSA-N 0.000 description 3
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- YNLAOSYQHBDIKW-UHFFFAOYSA-M diethylaluminium chloride Chemical compound CC[Al](Cl)CC YNLAOSYQHBDIKW-UHFFFAOYSA-M 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000007336 electrophilic substitution reaction Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 3
- GVNVAWHJIKLAGL-UHFFFAOYSA-N 2-(cyclohexen-1-yl)cyclohexan-1-one Chemical compound O=C1CCCCC1C1=CCCCC1 GVNVAWHJIKLAGL-UHFFFAOYSA-N 0.000 description 2
- 101150065749 Churc1 gene Proteins 0.000 description 2
- 101100388055 Mus musculus Polm gene Proteins 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 102100038239 Protein Churchill Human genes 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 241000219977 Vigna Species 0.000 description 2
- 235000010726 Vigna sinensis Nutrition 0.000 description 2
- 150000001336 alkenes Chemical group 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 229920005549 butyl rubber Polymers 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 150000001805 chlorine compounds Chemical group 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 125000003392 indanyl group Chemical group C1(CCC2=CC=CC=C12)* 0.000 description 2
- 239000003999 initiator Substances 0.000 description 2
- 229910052751 metal Chemical class 0.000 description 2
- 239000002184 metal Chemical class 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- 229920000620 organic polymer Polymers 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 230000000379 polymerizing effect Effects 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 125000003808 silyl group Chemical group [H][Si]([H])([H])[*] 0.000 description 2
- 239000003039 volatile agent Substances 0.000 description 2
- HGTUJZTUQFXBIH-UHFFFAOYSA-N (2,3-dimethyl-3-phenylbutan-2-yl)benzene Chemical group C=1C=CC=CC=1C(C)(C)C(C)(C)C1=CC=CC=C1 HGTUJZTUQFXBIH-UHFFFAOYSA-N 0.000 description 1
- KPZGRMZPZLOPBS-UHFFFAOYSA-N 1,3-dichloro-2,2-bis(chloromethyl)propane Chemical compound ClCC(CCl)(CCl)CCl KPZGRMZPZLOPBS-UHFFFAOYSA-N 0.000 description 1
- MJMQIMYDFATMEH-UHFFFAOYSA-N 2-chloro-2,4,4-trimethylpentane Chemical compound CC(C)(C)CC(C)(C)Cl MJMQIMYDFATMEH-UHFFFAOYSA-N 0.000 description 1
- OGFWWHDVONKVMA-UHFFFAOYSA-N CC(C)=C.CCCCCC Chemical group CC(C)=C.CCCCCC OGFWWHDVONKVMA-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- 239000004820 Pressure-sensitive adhesive Substances 0.000 description 1
- 229910018540 Si C Inorganic materials 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 125000005073 adamantyl group Chemical group C12(CC3CC(CC(C1)C3)C2)* 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 150000001343 alkyl silanes Chemical class 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- UWAXDPWQPGZNIO-UHFFFAOYSA-N benzylsilane Chemical compound [SiH3]CC1=CC=CC=C1 UWAXDPWQPGZNIO-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000001055 chewing effect Effects 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- PFBUKDPBVNJDEW-UHFFFAOYSA-N dichlorocarbene Chemical compound Cl[C]Cl PFBUKDPBVNJDEW-UHFFFAOYSA-N 0.000 description 1
- JGHYBJVUQGTEEB-UHFFFAOYSA-M dimethylalumanylium;chloride Chemical compound C[Al](C)Cl JGHYBJVUQGTEEB-UHFFFAOYSA-M 0.000 description 1
- ORVACBDINATSAR-UHFFFAOYSA-N dimethylaluminum Chemical compound C[Al]C ORVACBDINATSAR-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000012039 electrophile Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 229920001002 functional polymer Polymers 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- JQOAQUXIUNVRQW-UHFFFAOYSA-N hexane Chemical compound CCCCCC.CCCCCC JQOAQUXIUNVRQW-UHFFFAOYSA-N 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical group 0.000 description 1
- 238000005647 hydrohalogenation reaction Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000011968 lewis acid catalyst Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- JUHDUIDUEUEQND-UHFFFAOYSA-N methylium Chemical compound [CH3+] JUHDUIDUEUEQND-UHFFFAOYSA-N 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000012074 organic phase Substances 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 125000002524 organometallic group Chemical group 0.000 description 1
- 150000001282 organosilanes Chemical class 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 229920006294 polydialkylsiloxane Polymers 0.000 description 1
- LPNYRYFBWFDTMA-UHFFFAOYSA-N potassium tert-butoxide Chemical compound [K+].CC(C)(C)[O-] LPNYRYFBWFDTMA-UHFFFAOYSA-N 0.000 description 1
- 238000004382 potting Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- DNAJDTIOMGISDS-UHFFFAOYSA-N prop-2-enylsilane Chemical compound [SiH3]CC=C DNAJDTIOMGISDS-UHFFFAOYSA-N 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 239000000565 sealant Substances 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000010059 sulfur vulcanization Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000010189 synthetic method Methods 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- UKRDPEFKFJNXQM-UHFFFAOYSA-N vinylsilane Chemical compound [SiH3]C=C UKRDPEFKFJNXQM-UHFFFAOYSA-N 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000004383 yellowing Methods 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/54—Silicon-containing compounds
- C08K5/5403—Silicon-containing compounds containing no other elements than carbon or hydrogen
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/04—Monomers containing three or four carbon atoms
- C08F110/08—Butenes
- C08F110/10—Isobutene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/02—Alkylation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/26—Removing halogen atoms or halogen-containing groups from the molecule
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2810/00—Chemical modification of a polymer
- C08F2810/30—Chemical modification of a polymer leading to the formation or introduction of aliphatic or alicyclic unsaturated groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2810/00—Chemical modification of a polymer
- C08F2810/40—Chemical modification of a polymer taking place solely at one end or both ends of the polymer backbone, i.e. not in the side or lateral chains
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 最近の20年間に、種々の有機ケイ素化合物は種々の親電
子試薬と反応することが示された。反応は、ケイ素から
除去された1、2また3原子である多重結合を有する有
機ケイ素化合物、すなわちアリールシラン、ビニルシラ
ン、アルキニルシラン、シリル・エノール・エーテル、
アリルシラン、ベンジルシラン、ホモアリルシランおよ
び激しい条件下でのアルキルシランと生じる。これらの
反応の大部分はケイ素への中間カチオン・ベータへ導く
新電子攻撃によつて進行することをもくろんでいる。か
かる反応はカチオン安定化のために極めて位置選択的で
ある。シリル基は一般に後続の工程中に失われて、親電
子物質および予想できる位置に多重結合を有する化合物
を生じる。DETAILED DESCRIPTION OF THE INVENTION Industrial Application Over the last two decades, various organosilicon compounds have been shown to react with various electrophilic reagents. The reaction is carried out by removing organosilicon compounds having multiple bonds of 1, 2, or 3 atoms removed from silicon, that is, arylsilane, vinylsilane, alkynylsilane, silyl enol ether,
Formed with allylsilane, benzylsilane, homoallylsilane and alkylsilanes under violent conditions. Most of these reactions are expected to proceed by new electron attack on silicon leading to intermediate cation beta. Such reactions are highly regioselective due to cation stabilization. Silyl groups are generally lost during subsequent steps, resulting in electrophiles and compounds with multiple bonds at predictable positions.
有機ケイ素化合物の親電子置換は重合体合成における少
なくとも追求された合成法の1つである。比較的弱く分
極したSi−C結合のために、オルガノシランは弱い反応
性有機金属化合物として行動する。従つて、それらは他
の有機金属よりも便利に取り扱うことができる、すなわ
ち、それらは一般に無水または不活性雰囲気を必要とせ
ず、種々の官能基の存在下で不活性である。炭素原子に
比較的高い正電荷を帯びた炭素陽イオンまたは物質と有
機ケイ素化合物の親電子置換に関する研究は少ない。ア
ダマンチルおよび第三ブチル・ハロゲン化物は、ルイス
酸の存在下で選択の不飽和有機ケイ素化合物に置換する
ことが示された(例えば、I.Fleming et al.Synthesis,
1979,446;T.Sasaki et al.,J.Org Chem.,1980(45),35
59を参照)。Electrophilic substitution of organosilicon compounds is at least one of the pursued synthetic methods in polymer synthesis. Due to the relatively weakly polarized Si-C bonds, organosilanes behave as weakly reactive organometallic compounds. Therefore, they can be handled more conveniently than other organometallics, ie they generally do not require an anhydrous or inert atmosphere and are inert in the presence of various functional groups. There are few studies on electrophilic substitution between a carbon cation or a substance having a relatively high positive charge on a carbon atom and an organosilicon compound. Adamantyl and tert-butyl halides have been shown to displace selected unsaturated organosilicon compounds in the presence of Lewis acids (eg, I. Fleming et al. Synthesis,
1979, 446; T. Sasaki et al., J. Org Chem., 1980 (45), 35.
See 59).
発明が解決しようとする問題点 ポリイソブチレンは橋かけが困難であるので用途が限定
される。少量のイソプレンとの共重合は不飽和の残留位
置(サイト)を与え、従つて硫黄加硫をさせることが見
出された、そして第2次大戦中にブチル・ゴムの商品化
をもたらした。化学的およびオゾン不活性の外に、ブチ
ルゴムはガスに対して極低透過性であり、従つてタイヤ
チユーブに広く使用されている。低分子量のポリイソブ
チレン油は最近潤滑油の粘度を高めるために使用されて
おり、高分子量の非加硫化重合体は接着剤、コーク、シ
ーラント、および重合体添加剤に使用される。Problems to be Solved by the Invention Since polyisobutylene is difficult to crosslink, its use is limited. Copolymerization with small amounts of isoprene was found to give unsaturated residual sites, and thus sulfur vulcanization, and led to the commercialization of butyl rubber during World War II. In addition to being chemically and ozone inert, butyl rubber has an extremely low permeability to gases and is therefore widely used in tire tubes. Low molecular weight polyisobutylene oils have recently been used to increase the viscosity of lubricating oils and high molecular weight non-vulcanized polymers are used in adhesives, cokes, sealants, and polymer additives.
ポリイソブチレンとポリジアルキルシロキサン、いわゆ
るシリコーンとの共重は望ましい材料を生成する。驚く
ことに、ポリジメチルシロキサン(PDMS)とポリイソブ
チレンまたは他の有機重合体とのソフトブロツク−ソフ
トブロツク共重合体に関する研究は極めて少ない。かか
る共重合体は流体材料であることが期待される。くし型
構造のPDMSポリブタジエン・ソフトブロツク−ソフトブ
ロツク共重合体は、既知であるが、PIBシリコーン・ブ
ロツク共重合体が有する耐オゾン性および耐黄変性をも
たない。The co-weight of polyisobutylene and polydialkylsiloxane, so-called silicone, produces the desired material. Surprisingly, there are very few studies on soft block-soft block copolymers of polydimethylsiloxane (PDMS) with polyisobutylene or other organic polymers. Such copolymers are expected to be fluid materials. Comb type PDMS polybutadiene soft block-soft block copolymers are known but do not have the ozone resistance and yellowing resistance of PIB silicone block copolymers.
ポリジメチルシロキサン重合体を有機重合体に結合させ
てブロツク重合体を生成する簡単な方法は、最適には末
端オレフイン、H2C=CHRにSiH部分を白金触媒添加してS
iCH2CH2Rを生成するヒドロシリル化(hydrosilylatio
n)反応による方法である。A simple method to bond a polydimethylsiloxane polymer to an organic polymer to form a block polymer is optimally a terminal olefin, H 2 C = CHR with a platinum catalyst added to the SiH moiety to form a S
Hydrosilylation to produce iCH 2 CH 2 R
n) Method by reaction.
工業的には、イソブチレンは−100℃の如き低い反応温
度において塩化アルミニウムで重合される。その生成物
は大部分が飽和した脂肪族末端基を有する。Industrially, isobutylene is polymerized with aluminum chloride at low reaction temperatures such as -100 ° C. The product has predominantly saturated aliphatic end groups.
不飽和の位置を有するポリイソブチレン(PIB)はイソ
ブチレンと少量のイソプレンとの共重合によつて生成す
ることができる。得られる不飽和は加硫をさせるが、不
飽和の位置が主に内部であるため、ヒドロシリル化は抑
制または妨げられる。一端における末端オレフイン末端
基は、塩化アリルではなくてBCl3およびCH2=CHC(C
H3)2Clとの重合を開始させることによつて得られる。
高分子の他端は塩化物で終結される。CH2=CHC(CH3)
2−基が末端であるけれども、それは2つのメチル基に
よつて提供される立体障害のためにヒドロシリル化にお
いて反応性が全り強くない。その上、(AB)ブロツク共
重合体のみが生成する(ここでAはシリコーン・ブロツ
クを示し、Bは炭化水素ブロツクを示す)。もう1つの
方法は、BCl3と共にパラ塩化ジクミルのような特殊なジ
クロロカーボン共開始剤の使用、または共開始剤として
塩素を使用することによつてそれぞれの末端に塩素をも
つた重合体を作る方法である。その塩素末端重合体は次
に、カリウム第三ブトキシドで20時間還流し、冷却、3
回水洗し、乾燥することによつて脱ヒドロハロゲン化し
て−CH2−C(CH3)=CH2基を生成する(Kennedyによる
1982年8月3日付け米国特許第4,342,849号参照)。こ
の末端不飽和PIBは徐々にヒドロシリル化を受ける。ヒ
ドロシリル化は末端基が立体的に阻害されているので遅
い。従つて、両端で迅速なヒドロシリル化を受けて(A
B)Xブロツク共重合体(ここでxは2以上)を生成す
るCH2=CHCH2−PIB−CH2CH=CH2のような重合体を生成
するために、PIBに非障害アリル、CH2=CHCH2−、末端
官能性を提供する迅速、簡単かつ低コストの方法を提供
する必要がある。かかる材料は多くの用途、例えば電子
ポツテイング・ゲル、PIBをシリコーンと相溶性化する
界面活性剤、感圧接着剤および非粘着性チユーイング・
ガムとして有用である。Polyisobutylene (PIB) having unsaturated positions can be produced by copolymerization of isobutylene with a small amount of isoprene. The resulting unsaturation causes vulcanization, but the hydrosilylation is suppressed or prevented because the unsaturation site is predominantly internal. The terminal olefin terminal group at one end is BCl 3 and CH 2 ═CHC (C
It obtained Te cowpea to initiate the polymerization of the H 3) 2 Cl.
The other end of the polymer is terminated with chloride. CH 2 = CHC (CH 3 )
Although the 2 -group is terminal, it is not very reactive in hydrosilylation due to the steric hindrance provided by the two methyl groups. Moreover, only (AB) block copolymers are formed (where A represents a silicone block and B represents a hydrocarbon block). Another method is to use a special dichlorocarbon co-initiator such as dicumyl parachloride with BCl 3 or use chlorine as the co-initiator to make polymers with chlorine at each end. Is the way. The chlorine-terminated polymer is then refluxed with potassium tert-butoxide for 20 hours, cooled and
Turn washed with water, due to due to drying connexion with de-hydrohalogenation generating a -CH 2 -C (CH 3) = CH 2 group (Kennedy
See U.S. Pat. No. 4,342,849 issued Aug. 3, 1982). This terminally unsaturated PIB gradually undergoes hydrosilylation. Hydrosilylation is slow because the end groups are sterically hindered. Therefore, it undergoes rapid hydrosilylation at both ends (A
B) X block copolymer (where x is to produce a CH 2 = CHCH 2 polymers such as -PIB-CH 2 CH = CH 2 to generate two or more), non-failure allyl PIB, CH 2 = CHCH 2 -, quick to provide terminal functionality, there is a need to provide a simple and low cost method. Such materials have many applications, such as electronic potting gels, surfactants that make PIB compatible with silicones, pressure sensitive adhesives and non-sticking chewing agents.
It is useful as a gum.
問題点を解決するための手段 本発明は、求電子置換による第三クロロ・キヤツプド・
ポリイソブチレン(PIB)のアリルトリメチルシランで
のアリル化によつてアリル末端ポリイソブチレンを調製
する方法に関する。その合成は重合化学におけるシリル
・シンソン・アリルトリメチルシラン使用の最初の例で
ある。合成は、イソブチレンのBCl3触媒化モノーまたは
オリゴー第三塩化物「イニフアー(inifer)」開始重合
により始まり、続いて同一反応容器にヘキサン、アリル
トリメチルシランおよびTiCl4を添加する。この方法に
よつてアリル末端PIBが生成される。Means for Solving the Problems The present invention provides a tertiary chloro-capped
It relates to a method for preparing allyl-terminated polyisobutylene by allylation of polyisobutylene (PIB) with allyltrimethylsilane. Its synthesis is the first example of the use of silyl cinson allyltrimethylsilane in polymerization chemistry. Synthesis begins by BCl 3 catalyzed mono- or oligo-tertiary chloride "Inifua (inifer)" initiated polymerization of isobutylene, followed the addition of hexane, allyltrimethylsilane and TiCl 4 in the same reaction vessel. This method produces an allyl-terminated PIB.
本発明は、アリル基のような末端不飽和を有するポリイ
ソブチレンの如き新規の末端官能性重合体の合成法に関
する。本発明法の実施には、最初に単量体の重合を含む
塩素官能性または塩素/オレフインの混合官能性テレキ
リ(telechelic)官能性イソブチレン、および同時に開
始重合ができかつトランスフアー剤として作用する多官
能性化合物で始める必要がある。この化合物に対して、
用語「イニフアー」を用いているが、これは開示剤(in
itiator)とトランスフアー(transfer)に由来する。
イニフアーは一般にモノまたはオリゴー第三有機塩化
物、例えば(ClC(CH3)2C)XC6H(6-X)(式中のx=
1、2または3)である、またはイニフアーはH2C=CH
(CH3)2CClのようなクロロ・オレフインである。The present invention relates to a process for the synthesis of novel end-functional polymers such as polyisobutylene having terminal unsaturation such as allyl groups. In practicing the method of the present invention, chlorine-functional or mixed chlorine / olephine-functional telechelic-functional isobutylenes, which initially involve the polymerization of monomers, and a multiplicity of simultaneous initiating polymerizations and acting as transfer agents. It is necessary to start with a functional compound. For this compound,
We use the term “Inifur”, which is a disclosure agent (in
itiator) and transfer.
Inifers are generally mono- or oligo-tertiary organic chlorides such as (ClC (CH 3 ) 2 C) X C 6 H (6-X) (where x =
1, 2 or 3) or the inifer is H 2 C = CH
It is a chloro olefin such as (CH 3 ) 2 CCl.
従つて、本発明の目的は新規のテレキリ(telecheli)
アリル末端ポリイソブチレン重合体を提供することであ
る。本発明のもう1つの目的は、アリル不飽和の末端位
置をもつポリイソブチレンの合成法を提供することであ
る。Therefore, the object of the present invention is to provide a new telecheli.
It is to provide an allyl-terminated polyisobutylene polymer. Another object of the present invention is to provide a method for the synthesis of polyisobutylene having an allyl unsaturated terminal position.
本発明は、1つの反応器で2工程法において求電子置換
による第三クロロ末端キヤツプドPIBのアリルトリメチ
ルシランでのアリル化によるアリル末端PIBの調製法に
関する。本発明における「第三クロロ末端キヤツプドPI
B」または「第三塩素化ポリイソブチレン」は塩素原子
が結合している少なくとも1つの第三炭素原子を有する
ポリイソブチレン分子を意味する。さらに本発明は、PI
BのプレポリマーがBCl3とイニフアーの存在下でイニフ
アー法によつてイソブチレン(IB)から調製される方法
に関する。IBをPIBに重合することによつて得られる反
応混合体は急冷しないで、アリルトリメチルシランとフ
リーデルークラフツ型ルイス酸触媒、望ましくはTiCl4
との混合物を過剰に添加する。第三クロロ末端基に対し
て、IBの重合で残留する3倍(モル)過剰のBCl3がEt2A
lClのアリル化活性を完全に破壊し、SnCl4のアリル化活
性を著しく低下させる。これに対して、TiCl4のアリル
化効率は本発明によるBCl3の存在によつて悪影響を受け
ない。BCl3と塩化ジクミル・イニフアーで調製された低
分子量(Mn=1,000〜4,000)のPIBは、ルイス酸の存在
下で分子内シクロアルキル化を受けてインダニル末端基
を生じるモノ反応末端を10〜30%含みうる。しかしなが
ら、本発明によつて、完全末端アルキル化およびインダ
ニル末端基の生成がないことで、第三クロロ末端キヤツ
プド基に対して化学量論的にモルで2〜3倍過剰のアリ
ルトリメチルシランおよびTiCl4を使用することが達成
された。この方法によつてアリル末端PIB重合体を単離
することができる。The present invention relates to a process for preparing an allyl-terminated PIB by allylation of a third chloro-terminated capped PIB with allyltrimethylsilane by electrophilic substitution in a one-reactor, two-step process. In the present invention, "the third chloro-terminal capped PI
"B" or "tertiary chlorinated polyisobutylene" means a polyisobutylene molecule having at least one tertiary carbon atom to which a chlorine atom is attached. Furthermore, the present invention provides PI
A method in which the prepolymer of B is prepared from isobutylene (IB) by the inifer method in the presence of BCl 3 and inifer. The reaction mixture obtained by polymerizing IB into PIB was not quenched, but allyltrimethylsilane and Friedel-Crafts Lewis acid catalyst, preferably TiCl 4
The mixture with and is added in excess. The 3-fold (molar) excess of BCl 3 remaining in the polymerization of IB with respect to the tertiary chloro end group is Et 2 A.
It completely destroys the allylation activity of lCl and significantly reduces the allylation activity of SnCl 4 . In contrast, the allylation efficiency of TiCl 4 is not adversely affected by the presence of BCl 3 according to the invention. Low molecular weight (Mn = 1,000 to 4,000) PIBs prepared with BCl 3 and dicumyl chloride Inifer undergo 10 to 30 mono-reactive ends undergoing intramolecular cycloalkylation to give indanyl end groups in the presence of Lewis acids. % May be included. However, in accordance with the present invention, the absence of full-end alkylation and formation of indanyl end groups results in a stoichiometric molar excess of allyltrimethylsilane and TiCl 3 to tertiary chloro-terminated capped groups. Using 4 has been achieved. Allyl-terminated PIB polymers can be isolated by this method.
他の金属ハロゲン化物および金属錯体の使用は本発明の
範囲に含まれる。本発明において作用する他のフリーデ
ルークラフツ型ルイス酸金属触媒は、限定ではないがハ
ロゲン化ジルコニウム、ハロゲン化バナジウム、ハロゲ
ン化鉄および錯体、ハロゲン化アルミニウムおよびハロ
ゲン化アルミニウム・アルキルを含む。The use of other metal halides and metal complexes is within the scope of this invention. Other Friedel-Crafts Lewis acid metal catalysts that work in the present invention include, but are not limited to, zirconium halides, vanadium halides, iron halides and complexes, aluminum halides and aluminum alkyl halides.
さらに、本発明はアリル末端ポリイソブチレン重合体の
調製法に関し、該方法は三塩化ホウ素および四塩化チタ
ン、四塩化スズの存在下、または三塩化ホウ素の不在下
で限定ではないが塩化ジエチル・アルミニウムの存在下
で第三塩素化イソブチレンをアリルトリメチルシランと
反応させることによつてアリル末端ポリイソブチレン重
合体を生成することから成る。炭素原子1〜6を有する
アルキル基をもつた塩化アルキル・アルミニウムも本発
明に作用する。式▲R2 3▼SiCH2CR3CH2(式中のR2とR3
は水素から成る基および炭素原子1〜6を含有するアル
キル基から成る群からそれぞれ選ぶ)の置換アリルシラ
ンでのポリイソブチレンのアリル化は本発明の範囲に含
まれる。Further, the present invention relates to a process for preparing an allyl-terminated polyisobutylene polymer, which process includes but is not limited to boron trichloride and titanium tetrachloride, tin tetrachloride, or in the absence of boron trichloride, but not limited to diethyl aluminum chloride. Forming an allyl-terminated polyisobutylene polymer by reacting a trichlorinated isobutylene with allyltrimethylsilane in the presence of Alkyl aluminum chloride having an alkyl group having 1 to 6 carbon atoms also works in the present invention. Formula ▲ R 2 3 ▼ SiCH 2 CR 3 CH 2 (R 2 and R 3 in the formula
Is selected from the group consisting of groups consisting of hydrogen and alkyl groups containing 1 to 6 carbon atoms), and the allylation of polyisobutylene with substituted allylsilanes is within the scope of the present invention.
本発明はさらにアリル末端ポリイソブチレン重合体の調
製法に関する、そして該方法は、 (A)三塩化ホウ素とイニフアーの存在下で、塩化メチ
ルとヘキサンの混合体中においてイソブチレンを重合す
る工程、前記イニフアーは式AYn〔式中のAは1〜4の
リングを有する縮合および非縮合芳香族化合物、および
3〜20の炭素原子を有する線状および枝分れ脂肪族化合
物から成る群を選ぶ、Yは次式 によつて表される、但しRおよびR1はそれぞれアルキル
およびアリールから成る群から選び、Xは塩素および臭
素から成る群から選んだハロゲンである、そしてnは1
〜6の整数である〕を有する化合物から選ぶ; (B)得られた反応混合物のヘキサン濃度を上げて、重
合体の溶解度を改良する工程; (C)反応混合体にアリル官能性シランおよび四塩化チ
タンを添加することによつて、ポリイソブチレンをアリ
ル化する工程、ここでアリリ官能性シランは式▲R2 3▼
SiCH2CR3CH2〔式中のR2とR3はそれぞれ水素および1〜
6の炭素原子を有するアルキル基から成る群から選ぶ〕
を有する化合物から成る群から選ぶ; (D)前記アリル化反応を進めて、完了させる工程; (E)反応混合体を塩基性水溶液中に注入する工程;お
よび (F)アリル末端ポリイソブチレン重合体を単離および
精製する工程から成る。The present invention further relates to a process for preparing an allyl-terminated polyisobutylene polymer, which process comprises: (A) polymerizing isobutylene in a mixture of methyl chloride and hexane in the presence of boron trichloride and inifer. Is of the formula AYn [wherein A is selected from the group consisting of fused and unfused aromatic compounds having 1 to 4 rings, and linear and branched aliphatic compounds having 3 to 20 carbon atoms, Y is The following formula Embedded image wherein R and R 1 are each selected from the group consisting of alkyl and aryl, X is a halogen selected from the group consisting of chlorine and bromine, and n is 1
Is an integer of 6]; (B) increasing the hexane concentration of the resulting reaction mixture to improve the solubility of the polymer; (C) adding allyl-functional silane and tetrachloride to the reaction mixture. Allylating the polyisobutylene by adding titanium chloride, wherein the allyl functional silane is of the formula ▲ R 2 3 ▼
SiCH 2 CR 3 CH 2 (wherein R 2 and R 3 are hydrogen and 1 to
Selected from the group consisting of alkyl groups having 6 carbon atoms]
(D) a step of advancing and completing the allylation reaction; (E) a step of injecting the reaction mixture into a basic aqueous solution; and (F) an allyl-terminated polyisobutylene polymer. Is isolated and purified.
ここでの用語アリル化の「完了」とは、ポリイソブチレ
ンの主部がアリル化されるまで、アリル化反応を継続さ
せることを意味する。The term "completed" of allylation here means that the allylation reaction is continued until the main part of polyisobutylene is allylated.
2,4,4−トリメチル−2−クロロペンタン(TMP−Cl)の
アリル化に対するフリーデルークラフツ型ルイス酸の効
率は次の順序で低下することがわかつた: (CH3CH2)2AlCl>TiCl4>SnCl4≫BCl3 フリーデルークラフツ型ルイス酸の触媒活性における差
は反応温度が増す程増大した。温度を20℃から−70℃に
下げることによつて収率が増した。−70℃におけるアリ
ル化は、(CH3CH2)2AlCl、TiCl4またはSnCl4の存在下
で、第三クロロ末端キヤツプド基に対して2倍過剰(モ
ル)のアリルトリメチルシランを使用することによつて
定量的であつた。フリーデルークラフツ型ルイス酸によ
るイオン化の程度は置換収率を支配すると思われる。Ti
Cl4は、BCl3の存在下で第三塩素化ポリイソブチレンに
対して最も効率的なアリル化触媒であることが本発明に
よつて見出された。塩化ジエチルアルミニウムはBCl3の
不在下ではTiCl4よりも少し効率がよかつたけれども、
それはBCl3の存在下では不活性であつた。It was found that the efficiency of Friedel-Crafts Lewis acid for the allylation of 2,4,4-trimethyl-2-chloropentane (TMP-Cl) decreases in the following order: (CH 3 CH 2 ) 2 AlCl> The difference in catalytic activity of TiCl 4 > SnCl 4 >> BCl 3 Friedel-Crafts type Lewis acids increased as the reaction temperature increased. The yield was increased by lowering the temperature from 20 ° C to -70 ° C. Allylation at -70 ° C. uses a 2-fold excess (mole) of allyltrimethylsilane over the third chloro-terminated capped group in the presence of (CH 3 CH 2 ) 2 AlCl, TiCl 4 or SnCl 4. Therefore, it was quantitative. The degree of ionization by Friedel-Crafts type Lewis acid seems to control the substitution yield. Ti
It has been found according to the present invention that Cl 4 is the most efficient allylation catalyst for trichlorinated polyisobutylene in the presence of BCl 3 . Although diethylaluminum chloride was a little more efficient than TiCl 4 in the absence of BCl 3 ,
It was inactive in the presence of BCl 3 .
TMP−Clでのアリルトリメチルシランの親電子触媒反応
における劇的な溶媒作用も観察された。媒質の極性はCH
2Cl2、CH2Cl2とヘキサンの混合体および純ヘキサンの使
用によつて変つた。純ヘキサンにおけるモデル化合物TM
P−Clの場合、アリル化は著しく抑制されるけれども、
約30%CH2Cl2、70%ヘキサンまたは純CH2Cl2の存在下で
は、アリル化の効率は極めて高い。従つて、本発明の望
ましい実施例は「1反応容器2工程式」PIBのアリル化
であつて、IBをPIBに重合するために使用する約80%メ
チル/20%ヘキサンの反応媒体混合物は、ヘキサンを添
加することによつて約45:55のCH3Cl:ヘキサンに変る。
本発明のもう1つの望ましい実施態様はPIBの「2反応
容器2工程式」アリル化であつて、IBのPIBへの重合に
使用される80%塩化メチル/20%ヘキサン混合体が第2
工程において45:55のCH2Cl2:ヘキサンの溶媒組成に代
る。従つて、ヘキサンの濃度は55〜70重量%の範囲内の
濃度に高めることができる。A dramatic solvent effect in the electrophilic catalysis of allyltrimethylsilane with TMP-Cl was also observed. The polarity of the medium is CH
2 Cl 2, CH 2 Cl 2 and mixtures and HenTsuta Te cowpea to use pure hexane hexane. Model compound TM in pure hexane
In the case of P-Cl, the allylation is significantly suppressed,
In the presence of about 30% CH 2 Cl 2 , 70% hexane or pure CH 2 Cl 2 , the efficiency of allylation is extremely high. Accordingly, a preferred embodiment of the present invention is the allylation of a "one reaction vessel two step" PIB, wherein the reaction medium mixture of about 80% methyl / 20% hexane used to polymerize IB to PIB is: Addition of hexane converts to about 45:55 CH 3 Cl: hexane.
Another preferred embodiment of the present invention is a "two-reactor two-step" allylation of PIB, which comprises a second mixture of 80% methyl chloride / 20% hexane used to polymerize IB into PIB.
The solvent composition of 45:55 CH 2 Cl 2 : hexane is substituted in the process. Therefore, the concentration of hexane can be increased to a concentration within the range of 55 to 70% by weight.
材 料 塩化ジエチルアルミニウム((CH3CH2)2AlCl)は、Eth
yl社(米国、ルイジアナ州Baton Rouge)から得た。三
塩化ホウ素(BCl3)はユニオンカーバイド社(米国、コ
ネチカツト州、ダンベリ)から得た。塩化チタン(TiCl
4)はアルドリツヒ社(米国、ウイスコン州、ミルウオ
ーキー)から入手した。塩化スズ(SnCl4)はフイツシ
ヤー社(米国、ペンシルバニア州、ピイツバーグ)から
入手した。アリルトリメチルシランはPetrarch System
社(米国、ペンシルバニア州、ブリストール)から入手
した。クロロPIBはケネデイらの半連続イニフアー法
(J.Polym.Sci.Polm.Chem.Ed.,18,1523,1980)によつて
調製した。Diethyl aluminum chloride ((CH 3 CH 2 ) 2 AlCl) is Eth
yl (Baton Rouge, Louisiana, USA). Boron trichloride (BCl 3 ) was obtained from Union Carbide Corporation (Danbury, CT, USA). Titanium chloride (TiCl
4 ) was obtained from Aldrich Corporation (Milwaukee, Wisconsin, USA). Tin chloride (SnCl 4) is Fuitsushiya over, Inc. (the United States, Pennsylvania, Piitsubagu) was obtained from. Allyltrimethylsilane is the Petrarch System
(Bristol, Pennsylvania, USA). Chloro PIB was prepared by the semi-continuous inifer method of J. Kennedy et al. (J. Polym. Sci. Polm. Chem. Ed., 18 , 1523, 1980).
実施例 実施例1:「1反応容器2工程式」クロロPIBのアリル化 培養管内において、0.000281モルの塩化パラージクミ
ル、0.00154モルのBCl3の塩化メチル80部とヘキサン20
部の溶液25mlにイソブチレン0.0224モルを通すことによ
つて−80℃で60分間イソブチレンを重合させた。1時間
後、その溶媒組成をヘキサンを添加することによつて4
5:55のCH3Cl:ヘキサンになるように変えた。反応を急冷
しないで、塩化クミルの第三クロロ基に対してモルで約
2倍過剰のアリルトリメチルシラン(0.00109モル)とT
iCl4(0.000702モル)を−80℃で同時に添加した。60分
後、その系を0℃において飽和NaHCO3の溶液に注入し
た。アリル化重合体はアセトンで沈殿させ、ろ過によつ
て単離し、乾燥そしてCCl4に溶解させた。プロトンNMR
スペクトルは98%ビス・アリル−PIBの生成を確認し
た。GPCは数平均分子量3700を示した。Examples Example 1: "1 reaction vessel 2-step process" Allylation of chloro PIB In a culture tube, 0.000281 mol of para-dicumyl chloride, 0.00154 mol of BCl 3 of 80 parts of methyl chloride and hexane 20 were added.
Isobutylene was polymerized for 60 minutes at -80 ° C by passing 0.0224 mol of isobutylene through 25 ml of a solution of part. After 1 hour, the solvent composition was adjusted to 4 by adding hexane.
Changed to 5:55 CH 3 Cl: Hexane. Without quenching the reaction, there was about a 2-fold molar excess of allyltrimethylsilane (0.00109 mol) and T with respect to the tertiary chloro group of cumyl chloride.
iCl 4 (0.000702 mol) was added simultaneously at −80 ° C. After 60 minutes, the system was poured at 0 ° C. into a solution of saturated NaHCO 3 . The allylated polymer was precipitated with acetone, isolated by filtration, dried and dissolved in CCl 4 . Proton NMR
The spectrum confirmed the formation of 98% bis-allyl-PIB. GPC showed a number average molecular weight of 3,700.
実施例2:単離および精製クロロPIBのアリル化 クロロPIBはケネデイらの半連続イニフアー法(J.Pol.S
ci.,Polm.Chem.Ed.,18,1523,1980)によつて調製した。
約0.5gの第三クロロ末端PIBを5mlのジクロロメタンに溶
解して、テフロン止めコツクを備えた50mlのガラス反応
器の入れた。第三クロロ末端基に対してモルで3〜5倍
過剰のアリルトリメチルシランを窒素雰囲気下、注入器
で添加した。反応は、窒素雰囲下モルで2〜3倍過剰の
TiCl4ルイス酸を注入器で添加することによつて開始し
た。均一な装入物を時々かくはんした、そして25〜75分
後の飽和NaHCO3溶液(25ml)に注入した。有機相を分離
し、無水MgSO4上で乾燥し、揮発物質は真空中で蒸発さ
せた。残留ポリマモは少量のヘキサン(約2ml)に溶解
させ、アセトンで沈殿させ、分離し、アセトンで洗浄、
そして揮発物質は真空中で一晩蒸発させることによつて
除去した。乾燥重合体はCCl4(20〜30%)に溶解させ、
プロトンNMR分析にかけて、アリルPIBの生成を確認し
た。Example 2: Allylation of isolated and purified chloro PIB Chloro PIB is a semi-continuous inifer method of Kennedy et al. (J. Pol.S.
ci., Polm. Chem. Ed., 18 , 1523, 1980).
About 0.5 g of the third chloro-terminated PIB was dissolved in 5 ml of dichloromethane and placed in a 50 ml glass reactor equipped with a Teflon stopcock. A 3-5 molar excess of allyltrimethylsilane with respect to the tertiary chloro end groups was added with a syringe under a nitrogen atmosphere. The reaction is carried out under a nitrogen atmosphere in a molar excess of 2-3 times.
It was started by adding TiCl 4 Lewis acid with a syringe. The homogeneous charge was occasionally stirred and poured into saturated NaHCO 3 solution (25 ml) after 25-75 min. The organic phase was separated, dried over anhydrous MgSO 4, volatiles were evaporated in vacuo. Dissolve the residual polymom in a small amount of hexane (about 2 ml), precipitate with acetone, separate, wash with acetone,
The volatiles were then removed by evaporation in vacuum overnight. Dissolve the dried polymer in CCl 4 (20-30%),
Proton NMR analysis confirmed the formation of allyl PIB.
実施例3:クロロPIBの本来の位置におけるアリル化 イソブチレンの重合は、培養管内において0.063モル/dm
3塩化クミル、0.065〜0.180モル/dm3のアリルトリメチ
ルシランおよび1.2モル/dm3のイソブチレンのかくはん
溶液22mlにBCl30.80mlを迅速に添加することによつて行
つた。その反応は予め急冷したメタノール数mlの添加に
よつて終結させ、沈殿したアリル末端PIB重合体を単離
した。Example 3: Allylation in situ of chloro PIB Polymerization of isobutylene was 0.063 mol / dm in culture tubes.
3 chloride cumyl, from 0.065 to 0.180 mol / dm 3 of allyltrimethylsilane and 1.2 mol / dm 3 of quickly due connexion KoTsuta to the addition of BCl 3 0.80 ml to stirred solution 22ml of isobutylene. The reaction was terminated by the addition of a few ml of prequenched methanol and the precipitated allyl-terminated PIB polymer was isolated.
実施例4:「2反応容器2工程式」クロロPIBのTiCl4触媒
アリル化 培養管において0.000562モルのパラー塩化ジクミル、0.
00308モルのBCl3の80部の塩化メチルと20部のヘキサン
との溶液25mlにイソブチレン(0.0224モル)を−80℃で
60分間通すことによつてイソブチレンを重合させた。1
時間後、その反応を終結し、クロロ−PIBを単離し、洗
浄して残留BCl3を除去した。次に、クロロ−PIB1.0gを4
5/55CH2Cl2/ヘキサンの溶媒組成物10mlに取つた。塩化
クミルの第三クロロ基に対してモルで4倍過剰のアリル
トリメチルシラン(0.00422モル)とTiCl4(0.00236モ
ル)を−80℃で同時に添加した。60分後、その系を0℃
の飽和NaHCO3(50ml)の溶液に注入した。アリル化重合
体をアセトンで沈殿させ、ろ過により単離し、乾燥そし
てCCl4に溶解させた。プロトンNMRスペクトルはビス・
アリル−PIBの生成を確認した。Example 4: In TiCl 4 catalyst allylation culture tubes "second reaction vessel 2 Scheme" Chloro PIB 0.000562 mol para chloride dicumyl 0.
00308 mol of BCl 3 in 80 ml of methyl chloride and 20 parts of hexane in 25 ml of isobutylene (0.0224 mol) at −80 ° C.
Isobutylene was polymerized by passing through for 60 minutes. 1
After time, to terminate the reaction, the chloro -PIB isolated and washed to remove residual BCl 3. Next, 4 g of chloro-PIB is added.
It was taken up in 10 ml of a solvent composition of 5/55 CH 2 Cl 2 / hexane. A 4-fold molar excess of allyltrimethylsilane (0.00422 mol) and TiCl 4 (0.00236 mol) was added simultaneously at −80 ° C. with respect to the tertiary chloro groups of cumyl chloride. After 60 minutes, bring the system to 0 ° C.
Was poured into a solution of saturated NaHCO 3 (50 ml). The allylated polymer was precipitated with acetone, isolated by filtration, dried and dissolved in CCl 4 . The proton NMR spectrum is
Generation of allyl-PIB was confirmed.
実施例5:「2反応器2工程式」クロロPIBの塩化ジメチ
ル・アルミニウム触媒アリル化 培養管において、0.0562のパラー塩化ジクミル、0.0030
8モルのBCI3の80部塩化メチルと20部のヘキサン溶液25m
lにイソブチレン(0.0224モル)を180で1時間かけて通
すことにより、イソブチレンを重合させた。1時間後、
その反応を終結させ、クロロ−PIBを単離し、洗浄して
全ての残留BCl3を除去した。次に、45/55CH3Cl/ヘキサ
ンの溶媒10mlにクロロ−PIB1.0gを取つた。塩化クミル
の第三クロロ基に対してモルで3倍過剰のアリルトリメ
チルシラン(0.00314モル)と塩化ジメチルアルミニウ
ム(0.00218モル)を−80℃で同時に添加した。60分
後、その系を0℃の飽和NaHCO3の溶液50mlに注入した。
アリル化重合体はアセトンで沈殿させ、ろ過により単離
し、乾燥そしてCCl4中に溶解させた。プロトンNMRスペ
クトルはビス・アリル−PIBの生成を確認した。Example 5: "2-reactor 2-step" dimethyl-aluminum chloride-catalyzed allylation of chloro PIB In a culture tube, 0.0562 para-dicumyl chloride, 0.0030
25 parts of a solution of 8 mol of BCI 3 in 80 parts of methyl chloride and 20 parts of hexane
Isobutylene was polymerized by passing isobutylene (0.0224 moles) through 180 at 180 for 1 hour. One hour later,
The reaction was terminated, the chloro -PIB isolated, to remove any residual BCl 3 and washed. Next, 1.0 g of chloro-PIB was taken in 10 ml of a solvent of 45/55 CH 3 Cl / hexane. A 3-fold molar excess of allyltrimethylsilane (0.00314 mol) and dimethylaluminum chloride (0.00218 mol) were added simultaneously at −80 ° C. with respect to the tertiary chloro groups of cumyl chloride. After 60 minutes, the system was poured into 50 ml of a saturated NaHCO 3 solution at 0 ° C.
The allylated polymer was precipitated with acetone, isolated by filtration, dried and dissolved in CCl 4 . Proton NMR spectra confirmed the formation of bis-allyl-PIB.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 アントニイ・ポツプ・ライト アメリカ合衆国ミシガン州ロデス・ジエフ アーソン・ロード7300 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Antonio Popp Wright 7300 Rodson Jief Aason Road, Michigan, USA
Claims (4)
で、第三塩素化ポリイソブチレンをアリルトリメチルシ
ランと反応させることによって、アリル末端ポリイソブ
チレン重合体を生成することから成る、アリル末端ポリ
イソブチレン重合体の製造法。1. An allyl-terminated polyisobutylene polymer comprising forming an allyl-terminated polyisobutylene polymer by reacting a trichlorinated polyisobutylene with allyltrimethylsilane in the presence of a Friedel-Crafts type Lewis acid. How to make a coalesce.
第三塩素化ポイソブチレンをアリルトリメチルシランと
反応させることによって、アリル末端ポリイソブチレン
重合体を生成することから成る、アリル末端ポリイソブ
チレン重合体の製造法。2. In the presence of titanium tetrachloride and boron trichloride,
A method of making an allyl-terminated polyisobutylene polymer comprising reacting a chlorinated poisobutylene with allyltrimethylsilane to produce an allyl-terminated polyisobutylene polymer.
ルコニウム、塩化鉄、塩化バナジウム、四塩化スズおよ
び炭素原子1〜6のアルキル基を有する塩化アルキルア
ルミニウムから成る群から選んだハロゲン化金属の存在
下で、第四塩素化ポリイソブチレンをアリルトリメチル
シランと反応させることによって、アリル末端ポリイソ
ブチレン重合体を生成することから成る、アリル末端ポ
リイソブチレン重合体の製造法。3. In the presence of a metal halide selected from the group consisting of titanium tetrachloride, aluminum chloride, zirconium chloride, iron chloride, vanadium chloride, tin tetrachloride and alkylaluminum chloride having an alkyl group of 1 to 6 carbon atoms. Wherein the quaternary chlorinated polyisobutylene is reacted with allyltrimethylsilane to produce an allyl terminated polyisobutylene polymer.
フアーは式AYnを有する化合物から選ぶ、但し式中のA
は1〜4のリングを有する縮合および非縮合芳香族化合
物、および炭素原子3〜20を有する線状および枝分れ脂
肪族化合物から成る群から選び、Yは次式 (但し、式中のRおよびR1はそれぞれアルキルおよびア
リールからなる群から選ぶ、Xは塩素と臭素から成る群
から選んだハロゲンである)によって表される、そして
nは1〜6の整数である〕の存在下で、塩化メチルとヘ
キサンの混合体中においてイソブチレンを重合させる工
程; (B)前記反応混合体のヘキサン濃度を上げる工程; (C)前記反応混合体へ、アリル官能性シラン〔該アリ
ル官能性シランは式▲R2 3▼SiCH2CR3CH2(式中のR2
とR3はそれぞれ水素および炭素原子1〜6を有するアル
キル基から成る群から選ぶ)を有する化合物から成る群
から選ぶ〕と、四塩化チタンを添加することによってポ
リイソブチレンをアリル化する工程; (D)該アリル化反応を進行させて完了させる工程; (E)得られた反応混合体を塩基性水溶液に注入する工
程;および (F)アリル末端ポリイソブチレン重合体を単離および
精製する工程、から成るアリル末端ポリイソブチイレン
重合体の製造法。4. (A) Boron trichloride and inifer [wherein the inifer is selected from compounds having the formula AYn, where A in the formula
Is selected from the group consisting of fused and non-fused aromatic compounds having 1 to 4 rings and linear and branched aliphatic compounds having 3 to 20 carbon atoms, and Y is (Wherein R and R 1 are each selected from the group consisting of alkyl and aryl, X is a halogen selected from the group consisting of chlorine and bromine), and n is an integer from 1 to 6. In a mixture of methyl chloride and hexane in the presence of [a], (B) increasing the hexane concentration of the reaction mixture; (C) adding an allyl-functional silane to the reaction mixture. The allyl-functional silane is represented by the formula ▲ R 2 3 ▼ SiCH 2 CR 3 CH 2 (wherein R 2
And R 3 are each selected from the group consisting of hydrogen and an alkyl group having 1 to 6 carbon atoms) and a step of allylating polyisobutylene by adding titanium tetrachloride; D) advancing and completing the allylation reaction; (E) injecting the obtained reaction mixture into a basic aqueous solution; and (F) isolating and purifying an allyl-terminated polyisobutylene polymer, A process for producing an allyl-terminated polyisobutylene polymer comprising
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US919529 | 1986-10-16 | ||
| US06/919,529 US4758631A (en) | 1986-10-16 | 1986-10-16 | Method of preparing allyl-terminated polyisobutylene |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63105005A JPS63105005A (en) | 1988-05-10 |
| JPH0753768B2 true JPH0753768B2 (en) | 1995-06-07 |
Family
ID=25442256
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62259867A Expired - Lifetime JPH0753768B2 (en) | 1986-10-16 | 1987-10-16 | Allyl-terminated polyisobutylene polymer and method for producing the same |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US4758631A (en) |
| EP (1) | EP0264214B1 (en) |
| JP (1) | JPH0753768B2 (en) |
| CA (1) | CA1296135C (en) |
| DE (1) | DE3786319T2 (en) |
Families Citing this family (64)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5247021A (en) * | 1989-06-06 | 1993-09-21 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Process for preparation of a polymer having reactive terminal group |
| WO1990015081A1 (en) * | 1989-06-06 | 1990-12-13 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Method of producing polymer terminated with reactive group |
| TW211019B (en) * | 1991-12-20 | 1993-08-11 | Shell Internat Res Schappej B V | |
| US5448000A (en) * | 1994-02-17 | 1995-09-05 | New Mexico Tech Research Foundation | End-quenching the living polymerization of isobutylene with acetyl sulfate |
| WO1995025754A1 (en) * | 1994-03-18 | 1995-09-28 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Method of isolating isobutylene polymer |
| JP3500152B2 (en) * | 1994-06-09 | 2004-02-23 | 鐘淵化学工業株式会社 | Method for producing isobutene-based polymer |
| EP0709403A1 (en) * | 1994-10-28 | 1996-05-01 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Curable composition for injection molding |
| US5580935A (en) * | 1995-01-13 | 1996-12-03 | Exxon Chemical Patents Inc. | Functionalized polymer and method to obtain functionalized polymer |
| US5523359A (en) * | 1995-01-13 | 1996-06-04 | Exxon Chemical Patents Inc. | Functionalized polymer and methods to obtain functionalized polymer |
| JP3806475B2 (en) * | 1996-02-08 | 2006-08-09 | 株式会社カネカ | Method for producing (meth) acrylic polymer having functional group at terminal |
| US5663245A (en) * | 1996-03-22 | 1997-09-02 | The University Of Akron | Star polymers having a well-defined siloxane core and multiple polyisobutylene arms and a method for the synthesis thereof |
| US5733998A (en) * | 1996-03-26 | 1998-03-31 | The University Of Akron | Method, dispersing agent and initiator for the dispersion polymerization of isobutylene |
| US5665823A (en) * | 1996-08-30 | 1997-09-09 | Dow Corning Corporation | Polyisobutylene polymers having acrylic functionality |
| CA2219508A1 (en) | 1996-10-31 | 1998-04-30 | Kaneka Corporation | Curable resin composition |
| CN1128164C (en) * | 1996-11-28 | 2003-11-19 | 钟渊化学工业株式会社 | Method for producing hydroxyl-terminated (meth) acrylic polymer |
| GB9713279D0 (en) * | 1997-06-25 | 1997-08-27 | Dow Corning | Process for making silyl endblocked polymers |
| US6348546B2 (en) | 1997-12-04 | 2002-02-19 | Kaneka Corporation | Alkenyl-containing isobutylene group block copolymer and process for producing it |
| JP3941988B2 (en) | 1997-12-04 | 2007-07-11 | 株式会社カネカ | Alkenyl group-containing isobutylene block copolymer and method for producing the same |
| GB9814211D0 (en) | 1998-07-01 | 1998-09-02 | Dow Corning Sa | Polysiloxane-polybutylene copolymers |
| CN1183619C (en) * | 1999-10-21 | 2005-01-05 | 松下电器产业株式会社 | Polymer electrolyte fuel cell |
| US6773758B2 (en) | 2000-05-17 | 2004-08-10 | Kaneka Corporation | Primer composition and bonding method |
| JP4543267B2 (en) * | 2000-05-17 | 2010-09-15 | 株式会社スリーボンド | Curable composition for fuel cell |
| JP4705279B2 (en) * | 2001-08-10 | 2011-06-22 | 株式会社カネカ | Thermoplastic elastomer composition |
| US7195720B2 (en) * | 2002-02-20 | 2007-03-27 | Kaneka Corporation | Curable composition for heat conductive material |
| JP2005519155A (en) * | 2002-03-04 | 2005-06-30 | ビーエーエスエフ アクチェンゲゼルシャフト | Method for producing isobutene polymer |
| US7018701B2 (en) * | 2002-06-06 | 2006-03-28 | Fuji Polymer Industries Co., Ltd. | Thermally conductive sheet and method for manufacturing the same |
| TWI263657B (en) * | 2002-12-23 | 2006-10-11 | Kaneka Corp | Thermoplastic elastomer composition |
| DE10303275A1 (en) | 2003-01-28 | 2004-07-29 | Basf Ag | Functionalization of isobutene polymers, useful for the production of polyurethanes, comprises reaction of at least one isobutene polymer having terminal unsaturation with a hydroboration agent |
| US6969744B2 (en) * | 2003-06-19 | 2005-11-29 | University Of Southern Mississippi | Living and quasiliving cationic telechelic polymers quenched by N-substituted pyrrole and methods for their preparation |
| AU2005277275B2 (en) * | 2004-08-20 | 2011-10-20 | Chevron Oronite Company Llc | Method for preparation of polyolefins containing exo-olefin chain ends |
| US7705090B2 (en) * | 2004-08-20 | 2010-04-27 | Chevron Oronite Company Llc | Method for preparing polyolefins containing a high percentage of exo-olefin chain ends |
| ATE509966T1 (en) * | 2004-08-20 | 2011-06-15 | Chevron Oronite Co | METHOD FOR PRODUCING POLYOLEFINS WITH EXO-OLEFIN CHAIN END |
| DE102005002722A1 (en) * | 2005-01-20 | 2006-08-03 | Basf Ag | Process for the preparation of polyisobutene |
| DE102005002772A1 (en) * | 2005-01-20 | 2006-08-03 | Basf Ag | Process for the preparation of polyisobutene |
| US7501476B2 (en) * | 2005-12-30 | 2009-03-10 | Chevron Oronite Company, Llc | Method for preparing polyolefins containing vinylidene end groups using azole compounds |
| US8013073B2 (en) * | 2005-12-30 | 2011-09-06 | Chevron Oronite Company Llc | Method for preparing polyolefins containing vinylidine end groups using nonaromatic heterocyclic compounds |
| US7816459B2 (en) * | 2005-12-30 | 2010-10-19 | Chevron Oronite Company Llc | Method for preparing polyolefins containing vinylidine end groups using polymeric nitrogen compounds |
| WO2007104711A1 (en) * | 2006-03-16 | 2007-09-20 | Basf Se | Method for the cationic polymerization of cationically polymerizable ethylenically unsaturated monomers in the presence of epoxy ethers |
| DE102007044933A1 (en) | 2006-09-20 | 2008-05-29 | Basf Se | Preparing isobutene polymer, useful e.g. as fuel additives, comprises polymerizing isobutene/isobutene containing monomeric mixture in the presence of Lewis acid, initiators and a compound e.g. orthocarbonic acid ester |
| JP4932576B2 (en) * | 2007-04-12 | 2012-05-16 | 株式会社カネカ | Method for producing isobutylene polymer |
| GB0707278D0 (en) * | 2007-04-16 | 2007-05-23 | Dow Corning | Condensation curable compositions having improved self adhesion to substrates |
| GB0707176D0 (en) * | 2007-04-16 | 2007-05-23 | Dow Corning | Hydrosilylation curable compositions |
| US8394897B2 (en) * | 2008-03-25 | 2013-03-12 | Chevron Oronite Company Llc | Production of vinylidene-terminated polyolefins via quenching with monosulfides |
| US20090258803A1 (en) * | 2008-04-14 | 2009-10-15 | Harrison James J | Copolymers made with quasi-living polyolefins and unsaturated acidic reagents, dispersants using same, and methods of making same |
| CN102015786B (en) | 2008-05-02 | 2015-05-13 | 巴斯夫欧洲公司 | Method and apparatus for the continuous polymerization of cationically polymerizable monomers |
| WO2009135876A1 (en) | 2008-05-07 | 2009-11-12 | Basf Se | α-OLEFIN/ISOBUTENE DIBLOCK COPOLYMERS |
| US8063154B2 (en) * | 2008-06-24 | 2011-11-22 | The University Of Southern Mississippi | Preparation of exo-olefin terminated polyolefins via quenching with alkoxysilanes or ethers |
| US20100016191A1 (en) * | 2008-07-18 | 2010-01-21 | Harrison James J | Copolymers Made With Allyl-Terminated Polyolefins And Unsaturated Acidic Reagents, Dispersants Using Same, and Methods of Making Same |
| US8133954B2 (en) | 2008-10-22 | 2012-03-13 | Chevron Oronite Company Llc | Production of vinylidene-terminated and sulfide-terminated telechelic polyolefins via quenching with disulfides |
| US8344073B2 (en) | 2009-01-16 | 2013-01-01 | The University Of Southern Mississippi | Functionalization of polyolefins with phenoxy derivatives |
| US8552122B2 (en) * | 2009-03-31 | 2013-10-08 | The University Of Southern Mississippi | Amine-terminated telechelic polymers and precursors thereto and methods for their preparation |
| US8585940B2 (en) * | 2009-05-08 | 2013-11-19 | Innolene Llc | Ocular lens |
| EP2436702B1 (en) | 2009-05-29 | 2014-12-17 | JX Nippon Oil & Energy Corporation | Isobutylene-based polymer and method for producing same |
| US8394898B2 (en) | 2009-07-31 | 2013-03-12 | The University Of Southern Mississippi | In situ formation of hydroxy chain end functional polyolefins |
| US8492491B2 (en) | 2010-06-10 | 2013-07-23 | Chevron Oronite Company Llc | Methods for producing telechelic polyolefins from terpene initiators |
| US8592527B2 (en) | 2010-06-14 | 2013-11-26 | University Of Southern Mississippi | Vinyl ether end-functionalized polyolefins |
| EP2634215B1 (en) | 2010-10-29 | 2017-03-22 | Kaneka Corporation | Isobutylene-based block copolymer composition |
| JP2012107096A (en) * | 2010-11-16 | 2012-06-07 | Kaneka Corp | Heat conductive curable resin composition and curable resin molded product |
| MX2013013609A (en) | 2011-05-23 | 2014-01-08 | Nissan Motor | Conductive film, current collector using same, battery and bipolar battery. |
| US8969484B2 (en) | 2011-07-08 | 2015-03-03 | Chevron Oronite Company Llc | Methods of producing mono- and multi-functional polymers from terpene-based initiators |
| WO2014025986A2 (en) * | 2012-08-10 | 2014-02-13 | The University Of Akron | Novel polyisobutylene-based thermoplastic elastomers |
| US9023970B2 (en) | 2012-10-12 | 2015-05-05 | Basf Se | Process for preparing polyisobutenes |
| KR20150070198A (en) | 2012-10-12 | 2015-06-24 | 바스프 에스이 | Method for producing polyisobutenes |
| US10329361B2 (en) | 2016-10-28 | 2019-06-25 | The University Of Akron | Quantitative preparation of allyl telechelic polyisobutylene under reflux conditions |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3830872A (en) * | 1971-09-01 | 1974-08-20 | Dart Ind Inc | Use of xylene in controlling melt flow of modified polyolefin compositions |
| US4342849A (en) * | 1979-09-10 | 1982-08-03 | The University Of Akron | Novel telechelic polymers and processes for the preparation thereof |
| US4276394A (en) * | 1979-09-10 | 1981-06-30 | The University Of Akron | Novel telechelic polymers, block copolymers and processes for the preparation thereof |
| US4316973A (en) * | 1979-09-10 | 1982-02-23 | The University Of Akron | Novel telechelic polymers and processes for the preparation thereof |
| US4529778A (en) * | 1981-12-11 | 1985-07-16 | Conoco Inc. | Preparation of modified aromatic moiety-containing polymers |
| US4532061A (en) * | 1983-09-08 | 1985-07-30 | Uniroyal, Inc. | Grafted polyalphaolefin polymers, method for its production and oils containing it |
| US4593071A (en) * | 1983-09-23 | 1986-06-03 | Union Carbide Corporation | Water-curable, silane modified ethylene polymers |
| US4661552A (en) * | 1984-10-02 | 1987-04-28 | Phillips Petroleum Company | Polymer composition and process |
-
1986
- 1986-10-16 US US06/919,529 patent/US4758631A/en not_active Expired - Lifetime
-
1987
- 1987-07-29 CA CA000543233A patent/CA1296135C/en not_active Expired - Lifetime
- 1987-10-05 DE DE87308791T patent/DE3786319T2/en not_active Expired - Lifetime
- 1987-10-05 EP EP87308791A patent/EP0264214B1/en not_active Expired - Lifetime
- 1987-10-16 JP JP62259867A patent/JPH0753768B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| EP0264214A2 (en) | 1988-04-20 |
| EP0264214A3 (en) | 1989-02-08 |
| JPS63105005A (en) | 1988-05-10 |
| DE3786319T2 (en) | 1993-12-09 |
| CA1296135C (en) | 1992-02-18 |
| DE3786319D1 (en) | 1993-07-29 |
| EP0264214B1 (en) | 1993-06-23 |
| US4758631A (en) | 1988-07-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH0753768B2 (en) | Allyl-terminated polyisobutylene polymer and method for producing the same | |
| US6194597B1 (en) | Living cationic polymers prepared from silyl-functional aromatic initiators | |
| US4143089A (en) | Silylated polymers | |
| CN111918896A (en) | Process for making block copolymer compositions | |
| US5981785A (en) | Silyl-functional initiator for living cationic polymerization | |
| JPH0995514A (en) | Production of silyl-terminated polyolefin | |
| JPWO1995033774A1 (en) | Method for producing isobutene polymer | |
| US6051657A (en) | Silyl-functional living cationic polymers | |
| JP3388865B2 (en) | Method for producing isobutylene polymer having olefin group | |
| JP2002348317A (en) | Method for producing isobutylene-based polymer | |
| JP2969470B2 (en) | Isobutylene polymer having allyl group at terminal and method for producing the same | |
| CA1290885C (en) | Group transfer polymerization catalyzed by mercury compounds | |
| JP3473862B2 (en) | Isobutylene-based polymer containing carbon-carbon unsaturated group and method for producing the same | |
| JP2700251B2 (en) | Method for producing isobutylene-based polymer having functional end | |
| EP0383566B1 (en) | Process for preparing organic silicon compounds | |
| CN100457791C (en) | Metal organic compound, catalyst composition containing same, and method for polymerizing isoolefin | |
| CN108699171B (en) | Monofunctional or telechelic copolymers of 1, 3-dienes with ethylene or alpha-monoolefins | |
| JP3631213B2 (en) | Ferrocenylene silylene polymer having a functional group and method for producing the same | |
| Hadjikyriacou et al. | Coupling and linking reactions of living polyisobutylene by allylsilanes | |
| US6087461A (en) | Process for making silyl endblocked organic polymers | |
| EP1620476A4 (en) | POLYMERIZATION OF I-BUTENE IN HYDROCARBON MEDIA USING BIS (BORANE) CO-INITIATORS | |
| JP3388880B2 (en) | Isobutylene polymer and method for producing the same | |
| JP3073252B2 (en) | Method for producing copolymer | |
| JPH0441684B2 (en) | ||
| JPH09124788A (en) | Polymerization initiator and polymerization method using the same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| EXPY | Cancellation because of completion of term | ||
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080607 Year of fee payment: 13 |